000 05898cam a2200673Ii 4500
001 ocn879676220
003 OCoLC
005 20230823095414.0
006 m o d
007 cr cnu---unuuu
008 140515s2014 enk ob 001 0 eng d
040 _aN$T
_beng
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019 _a880058644
_a880234226
020 _a9781118827000 (electronic bk.)
020 _a1118827007 (electronic bk.)
020 _a9781118827123 (electronic bk.)
020 _a1118827120 (electronic bk.)
020 _z9781848216501
020 _z1848216505
029 1 _aCHVBK
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029 1 _aCHBIS
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029 1 _aDEBSZ
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029 1 _aDEBBG
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035 _a(OCoLC)879676220
_z(OCoLC)880058644
_z(OCoLC)880234226
050 4 _aTP1175.E9
072 7 _aTEC
_x009010
_2bisacsh
082 0 4 _a668.413
_223
049 _aMAIN
245 0 0 _aPolymer extrusion /
_cedited by Pierre G. Lafleur, Bruno Vergnes.
264 1 _aLondon :
_bISTE-Wiley,
_c2014.
300 _a1 online resource (xii, 337 pages)
336 _atext
_btxt
_2rdacontent
337 _acomputer
_bc
_2rdamedia
338 _aonline resource
_bcr
_2rdacarrier
490 1 _aMaterials science series
504 _aIncludes bibliographical references and index.
588 _aDescription based on online resource; title from PDF title page (Wiley, viewed July 10, 2014)
505 0 _aCover; Title Page; Copyright; Table of Contents; Introduction; Chapter 1. Continuum Mechanics, Rheology and Heat Transfer Overview; 1.1. Continuum mechanics; 1.1.1. Strain; 1.1.2. Strain rate; 1.1.3. Stress; 1.1.4. General equations in continuum mechanics; 1.2. Rheology; 1.2.1. Newtonian behavior; 1.2.2. General viscous behavior; 1.2.3. Effects on pressure and temperature; 1.3. Heat transfer [CAR 59, BIR 60, AGA 14]; 1.3.1. The thermal balance equation; 1.3.2. Heat transfer during flow; 1.3.3. Cooling temperature; 1.4. Bibliography; Chapter 2. Calculation Methods; 2.1. Introduction.
505 8 _a2.2. 1D solutions2.2.1. Isothermal calculation; 2.2.2. Non-isothermal calculations; 2.3. 2D solutions; 2.3.1. Network method (or FAN method); 2.3.2. Finite element method; 2.4. Bibliography; Chapter 3. Single-Screw Extrusion; 3.1. Introduction; 3.2. Geomentry and approximations; 3.3. Solid conveying zone; 3.3.1. Phenomenological description; 3.3.2. Modeling; 3.3.3. Synthesis; 3.3.4. Determination of physical parameters; 3.4. Melting zone; 3.4.1. Phenomenological description; 3.4.2. Modeling; 3.5. Metering zone; 3.5.1. Phenomenological description; 3.5.2. Modeling; 3.6. Overall model.
505 8 _a3.7. Technological improvements3.7.1. Grooved barrels; 3.7.2. Barrier screws; 3.7.3. Mixing heads; 3.8. Conclusion; 3.9. Bibliography; Chapter 4. Co-rotating Twin-Screw Extrusion; 4.1. Twin-screw extrusion; 4.1.1. The different types of extruders; 4.1.2. Different flow types; 4.2. General overview of co-rotating twin-screw extruders; 4.2.1. Characteristic features of co-rotating twin-screw extruders; 4.2.2. Geometry of the screws and barrel; 4.2.3. Conventional approximations; 4.3. Solid conveying zone; 4.4. Melting zone; 4.4.1. Experimental studies; 4.4.2. Theoretical models.
505 8 _a4.5. Flow in the molten state4.5.1. Right- and left-handed screw element; 4.5.2. Mixing elements; 4.5.3. Heat transfer; 4.5.4. Residence time distribution; 4.6. An overall model of twin-screw extrusion; 4.6.1. General description; 4.6.2. Calculation algorithm; 4.6.3. Residence time distribution; 4.6.4. Example of results using the LUDOVIC© software; 4.7. Compounding application and production of complex materials; 4.7.1. Compounding and mixing; 4.7.2. Reactive extrusion; 4.7.3. Polymer blends; 4.7.4. Production of clay-based nanocomposites; 4.7.5. Optimization and scale-up; 4.8. Conclusion.
505 8 _a4.9. BibliographyChapter 5. Profile Extrusion; 5.1. Profile extrusion; 5.1.1 Different types of profile dies; 5.1.2. Flow calculation inside profile dies; 5.1.3. Evaluation of post-extrusion phenomena; 5.1.4. Design of extrusion dies; 5.2. Pipe extrusion; 5.2.1. Introduction; 5.2.2. Flow calculation; 5.3. Calibrators; 5.3.1. Friction calibrators; 5.3.2. External compressed air calibrators; 5.3.3. External vacuum calibrators; 5.3.4. Internal calibrators; 5.4. Conclusion; 5.5. Bibliography; Chapter 6. Production of Films and Sheets; 6.1. Introduction; 6.2. Cast film extrusion; 6.2.1. Processing.
520 _aExtrusion is by far the most important and the oldest processing and shaping method for thermoplastic polymers. This process concerns almost all synthetic polymers, as well as elastomers or food materials. Single-screw extrusion is mainly used nowadays to manufacture finished goods or semi-finished products. More than 90 million tons of thermoplastics are therefore processed every year. Twin-screw extrusion may be divided into two systems: contra-rotating systems used within the context of PVC extrusion, for the manufacture of pipes or profiles; and co-rotating systems experiencing nowa.
650 0 _aPolymers
_xExtrusion.
650 7 _aTECHNOLOGY & ENGINEERING / Chemical & Biochemical
_2bisacsh
650 7 _aPolymers
_xExtrusion.
_2fast
_0(OCoLC)fst01070614
650 4 _aPlastics
_xExtrusion.
650 4 _aPlastics.
655 4 _aElectronic books.
655 0 _aElectronic books.
700 1 _aLafleur, Pierre G.,
_d1957-
_eeditor.
700 1 _aVergnes, Bruno,
_eeditor.
776 0 8 _iPrint version:
_aLafleur, Pierre G.
_sExtrusion des polymères. English.
_tPolymer extrusion.
_dLondon : ISTE, 2014
_z9781848216501
_w(OCoLC)879401189
830 0 _aMaterials science series (London, England)
856 4 0 _uhttp://dx.doi.org/10.1002/9781118827123
_zWiley Online Library
994 _a92
_bDG1
999 _c21389
_d21348
526 _bps